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Rechargeable alkaline manganese cell with cathode consistency compensation

a technology of cathode consistency and alkaline manganese, which is applied in the direction of cell components, primary cell maintenance/service, sustainable manufacturing/processing, etc., can solve the problems of reducing the quantity of active cathode components, affecting cell performance, and excessive pellet breakage, so as to increase the charging efficiency and cumulative cell capacity of rechargeable alkaline cells, prevent damage to the cell, and increase the cell capacity

Active Publication Date: 2005-07-28
BLIZZARD TECH INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0014] The present invention advantageously provides a cathode with an acceptable consistency when pressed and formed into a cathode pellet, without noticeably decreasing the electrical performance of the cells made using the pellet.
[0019] The charge methodology of the present invention advantageously results in increased charging efficiency and cumulative cell capacity of rechargeable alkaline cells in a safe and automatable manner. Approximately a 15% increase in cell capacity may be obtained. A current pulse may be permitted to pass through the cell only if the no-load voltage does not exceed the first charge voltage to prevent damage to the cell through overcharging. The first charge voltage may be 1.75 V. The current pulse may have a duration of 14.5 seconds. The pre-determined time interval may be 0.5 seconds.

Problems solved by technology

Without the addition of sufficient binder (typically about 1.0-2.0% by weight) excessive pellet breakage occurs during automated production.
The addition of a binder has an adverse impact on cell performance; since binders are electrochemically inactive, the presence of the binder reduces the quantity of active cathode components, such as manganese dioxide, that are available to participate in electrochemical reactions.
Also, binders are typically non-conductive.
Lower concentration is not effective in achieving the aforementioned advantages.
The addition of a binder to these cells is undesirable, since the presence of the binder reduces cell performance.
In fact, when barium compounds such as BaO or Ba(OH)2*8H2O are used as additives, the formed pellets exhibit a “sticky” consistency that impedes continuous processing.
As a result, the improved cathode formulations cannot be used in a continuous production environment, making batteries with these formulations too expensive for the end-user.
Although binders are used to increase flexural strength of the cathode as an aid in continuous pellet processing, binders are not normally selected to modify the consistency of the cathode pellet.
Rechargeable alkaline cells are prone to cell failures when overcharging takes place.
Overcharge results in damage to cell components and will cause increased internal gassing, which in turn may eventually cause the cell to fail from electrolyte leakage due to overpressure.
However, a portion of the cell's capacity is not re-charged, which results in a loss of available performance.
The loss of available performance is especially significant when inert materials such as additives or binders are added to the cathode, as the presence of these materials reduces the amount of active cathode component available for electrochemical reaction.

Method used

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Experimental program
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Effect test

first embodiment

[0031] In a first embodiment, a charge current of 300-350 mA is applied. The charge frequency is one pulse every 15 seconds having a duration of 14.5 seconds, or 4 pulses / minute. The measurement frequency is equal to the charge frequency (4 measurements / minute), but offset by a no-load time interval of 0.5 seconds from each charge pulse. In a first charging phase, the first threshold voltage is 1.75 V. When the no-load voltage is equal to or greater than the first threshold voltage, the next subsequent pulse in the series of pulses defined by the charging frequency is skipped. The next measurement is taken at the usual time, as if the pulse had not been skipped. When the ratio of pulses to skipped pulses is 1:6, the first charging phase ends. Normally, the ratio of 1:6 is attained when six skipped pulses are counted consecutively.

[0032] The charging method may utilize any number of discrete charging phases. In a second embodiment there are two charging phases and in a third embodime...

third embodiment

[0055] The control and the cells according to the present invention were subjected to 25 discharge-charge cycles. Each cycle consisted of discharge using a 10 ohm resistive load to discharge the cells to a cut-off voltage of 0.9V followed by charging according to either the standard charge method or the new charge method. The standard charge method consisted of charging for 12 hours to a voltage limit of 1.65 V with an initial charge current of approx. 400 mA applied continuously. As the cell voltage increases, the actual charge current decreases and tapers off to almost zero as the 1.65 V limit is reached, hence this method is also referred to as ‘taper’ charge. The new charge method was as described above, also conducted for 12 hours.

[0056] Table 3 shows the capacity of the 25th cycle and the cumulative capacity over 25 cycles for all cells indicating the percentage changes of the different charge methods. The term cumulative capacity means the sum of all individual discharge cap...

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Abstract

In an improved rechargeable alkaline manganese cell that has a manganese dioxide cathode comprising pellets formed by pressing a cathode powder blend comprising a hygroscopic additive for increasing cumulative capacity, the sticky consistency of the pellets, which is un-desirable for continuous automated production is compensated for by the addition of up to 0.5% of a hydrophobic binder. This small amount leaves the cell performance substantially unimpaired, but provides the desired consistency for large-scale production. Further disclosed is an improved charge methodology for a rechargeable alkaline manganese cell wherein the charge current is pulsed at a voltage in excess of 1.65 V and the no-load cell voltage response is monitored at predetermined intervals. No charge current pulse is permitted to pass through the cell if the no-load voltage exceeds a threshold value. This results in increased utilization of the capacity of the cell while reducing the likelihood of damage to the cell due to overcharging.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS [0001] This application claims the benefit of U.S. patent application 60 / 537,900, filed Jan. 22, 2004.FIELD OF THE INVENTION [0002] The invention relates to rechargeable alkaline batteries. Specifically, the invention relates to cathode formulations of such batteries that comprise a hydrophobic cathode additive for affecting the consistency of pressed cathode pellets to make them more amenable to continuous production. The invention also relates to an improved charging method for use with rechargeable alkaline manganese cells, particularly the cells of the present invention. BACKGROUND OF THE INVENTION [0003] Alkaline battery technology has been used since the 1970's to provide inexpensive, long-lasting portable power sources for a variety of electrical applications. Disposable alkaline batteries, or primary cells are the most common example. However, due to recent technical advancements, re-chargeable alkaline batteries, or secondary cells, h...

Claims

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Application Information

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IPC IPC(8): H01M4/04H01M4/24H01M4/26H01M4/50H01M4/62H01M10/24H01M10/28H02J7/00
CPCH01M4/043H01M4/24H01M4/26H01M4/30Y02E60/124H01M4/621H01M10/24H01M10/44H01M4/50Y02E60/10Y02P70/50
Inventor DANIEL-IVAD, JOSEF
Owner BLIZZARD TECH INC